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In the study, PP/PTFE composites with different degree of fibrillation are prepared. Crystallization and rheology behavior are investigated. PTFE is easily deformed into fiber during compounding. The presence of PTFE fiber enhances the kinetics of isothermal crystallization of PP. The second modulus plateau at the low ω and a tan δ peak indicate the existence of a three dimensional networks. Extrusion foaming results show a 2 orders increase in cell density and 10-fold decrease in expansion ratio due to addition of PTFE compared to that of PP. With PTFE nanofiber, open-cell content of the composites is increased.
We researched a novel simulation strategy that predicts bubble growth phenomenon tailored to high-pressure foam injection molding (HP-FIM) processes. This was done via systematic HP-FIM experiments using a visualization technique. The mathematical model that we developed was based on the well-known “cell model”. To improve the model’s robustness and accuracy, we used the Simha-Somcynsky equation of state for the PS/CO2 mixture, which in turn offers an accurate prediction of the initial bubble radius. Moreover, to capture the fluid flow and mass transport behavior during bubble growth, the transport and rheological properties (that is, its diffusion coefficient, surface tension, viscosity, and relaxation time) that were adopted in this work were functions of the temperature, the pressure, and the gas concentration. In this work, instead of solving the cavity temperature and pressure separately, the temperature and pressure profile inside the cavity were respectively simulated using MoldFlow and experimentally obtained. By inputting the initial gas concentration and the transient pressure and temperature profiles, the proposed model could accurately predict the bubble growth profile under different HP-FIM conditions. The proposed model was validated using experimental data obtained from a series of visualized HP-FIM trials. In both cases, qualitative and good quantitative agreements were achieved between the simulated and the measured bubble growth data.
The strain hardening behavior of polymers has important roles in processing such as foaming, film formation, and fiber spinning. The most common method to enhance strain hardening is to introduce a long-chain branching structure on the backbone of a linear polymer, but this method is costly and challenging to tailor the behavior. We hypothesized that in situ shrinking fibers can increase the strain hardening of linear polymers, and the degree can be efficiently controlled. In this study, we show that heat-activated shrinking fibers compounded in linear polypropylene enhance strain hardening and foamability. Moreover, changing processing conditions, such as temperature, can amplify the degree of enhancement. Rheological measurements and physical foaming tests are shown to support our hypothesis.
Shear stress on polymers has been shown to have a strong effect on morphological and thus mechanical properties of the final structure. In this study, an in-situ visualization system was developed to i) visualize crystal nucleation and growth with high spatial and temporal resolutions and ii) have capability to measure the local shear stress and viscosity of a saturated polymer in isolated, simple shear. The system allows for easy control of experimental parameters: applied shear strain, shear strain rate, temperature, heating/cooling rate, pressure, polymer, and saturation gas. An early verification of the shear stress measuring capability was conducted of the This visualization/measuring system provides a reliable way of determining both rheological and optical properties of plastics simulated under dynamic conditions like that of industrial plastic processes.
Thermo-rheological testing is important for the vinyl industry, as it indicates the temperature range over which a given vinyl formulation can be used in a specific application. A test that has been used for many years is described in D1043, the Clash-Berg stiffness test. The test typically consists of determining at what temperature a material will have a shear modulus of 310.3 MPa (45,000 psi) after 5 seconds of stress applied in torsion. The instrumentation that is used for this test is antiquated and has become difficult to procure. Modern rotational rheometers are well-suited for this test and can be considered as replacements for the older equipment. In this presentation, we will show test results from Clash-Berg tests on TA Instruments DHR rotational rheometer and will demonstrate the excellent correlation between results from the rotational rheometer and the torsion tester.
It is widely accepted that the manufacturing of high expansion PP foams with fine cell morphology is a challenging task due to the low melt strength and the weak rheological behavior of the linear polypropylene. In this study we present a novel method to manufacture high cell density, large expansion microcellular foam through nano-fibrilation PP/PET composites. Various studies have been conducted to improve the processability of linear PP foams. Until now, the most successful industrial approach is using the branching PP as it expressed the strain hardening response and the increased melt strength behavior. However, the commercial price of branching PP resins are still doubled or even tripled comparing with linear PP resins, which dramatically limits the branching PP’s applications. Inducing chemical cross-linking is proven to be another effective way to improve the melt strength of PP. However, the cross-linked structure causes difficulty in recycling PP resins. Furthermore, the cross-linking reaction is not evenly initiated throughout the matrix rendering non-uniform cell structure in the final foam product. Implementing inorganic/organic filler is another alternative route for enhancing the foamability. PP reinforced with those fillers has higher viscosity and better elasticity at melting state. Nonetheless, the well-recognized challenging issue is to achieve well distribution and dispersion of nano-size fibers inside the polymer matrix. Because of the large surface to volume ratio, the nano-fibers tend to agglomerate. The well-established methods usually requires complex experimental conditions and normally involves dealing with chemical hazards. By implementing nano-fibrillation technology, all above mentioned draw-backs were overcome. The nano-fibrillation technology is used to manufacture polymer-polymer fibril composite in this study. The nano-fibrillation technology can generate high aspect ratio nano-fibrils uniformly dispersed inside the polymer matrix. The processing can be briefly summarized as: (i) blending immiscible polymer matrix (A) and polymer reinforcement (B) to make polymer (B) dispersed in spherical shape (the melting temperature of polymer B should be at least 30oC higher than polymer A); (ii) applying large deformation on the polymer extrudate by either hot stretching or cold stretching; (iii) carefully choosing a temperature between the melting temperature of polymer A and polymer B to melt the composite without damaging the fibril morphology of polymer B. In this study, three kinds of PPs with different viscosity are reinforced with PET nano-fibrils via melt spinning. The study shows that the high viscosity PP is preferred to generate low diameter nano-fibrils (~200 nm) in a wide concentration range; while the diameter of fibrils in low viscosity PP decreased with raising PET concentration. The oscillatory shear behavior is studied by comparing the storage modulus (G’) and phase angle (tanδ) of the non-fibrillated and fibrillated samples. Differential scanning calorimetry and birefringence optical microscope were employed to study the crystallization kinetics of PP/PET fibril composites. The rheological properties and crystallization kinetics were significantly improved with the presence of PET fibrils. Crucially, benefit from the strengthened rheological behavior and crystallization kinetics, the batch foaming of PP/PET nano-fibril composite is able to product a high cell density polymer foams.
The present work was conducted to assess the influence of polymer viscosity variation from batch to batch on the part dimensions and production interruptions. The results show however that parameters such as mold temperature, barrel temperature profile and holding pressure have much more influence on these two production quality indicators than the polymer viscosity.
This work focuses on exploring the long-term rheological behavior of polylactic acid and its nano-composites containing 3% clay. Creep and recovery experiments were performed at 160°C for the neat PLA and its composite. Zero-shear rate viscosity was determined and used to determine the terminal relaxation time. Also, the continuous retardation spectra were calculated from the creep data and found to be consistent with those from the oscillatory data.
Antioxidants (AO) are used to protect the polymer from deterioration either during extrusion or after production. Probably two types of Antioxidants are used to protect polymer, primary antioxidant (phenol type) and secondary antioxidant (phosphate type). The performance ratio of both the antioxidants is depend on its process technology, processing conditions and its application. To understand the effect of each antioxidants on HomoPP, different samples at different AO dosage were extruded. Relevant product properties such as mechanical, physical and rheology were measured. The test result obtained elucidates that the polymer recipe is a balance of additives to meet the requisite end product properties under the employed processing conditions.
The objective of this work is to study the variations of how independent processing parameters such as temperature, speed, and feed rate affect the dependent responses for consistent output colour (L*, a*, b*, dE*). In this study, the compounded material was processed on an intermeshing twin-screw extruder (TSE) and injection molded to evaluate their effect on the colour stability, rheology and dispersion of the polycarbonate resins. Focus was extended to the interaction of the speed, which correlates to the dispersion and colour changes.
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Any article that is cited in another manuscript or other work is required to use the correct reference style. Below is an example of the reference style for SPE articles:
Brown, H. L. and Jones, D. H. 2016, May.
"Insert title of paper here in quotes,"
ANTEC 2016 - Indianapolis, Indiana, USA May 23-25, 2016. [On-line].
Society of Plastics Engineers
Note: if there are more than three authors you may use the first author's name and et al. EG Brown, H. L. et al.